METHODE POUR DETERMINER LE NIVEAU D'UNE CHARGE DE KEROSENE DANS UNE INSTALLATION DE CRAQUAGE THERMIQUE

METHOD OF DETERMINING LIQUID LEVEL OF CHARGE STOCK IN THERMAL CRACKING UNIT

Abrégé anglais

IMPROVED METHOD OF DETERMINING LIQUID LEVEL
OF CHARGE STOCK IN THERMAL CRACKING UNIT
ABSTRACT OF THE DISCLOSURE
An improved method is described for determining the
liquid level of a heavy petroleum oil charge stock, e.g. a
refinery processing residue, in a thermal cracking unit by
measuring the liquid pressure at a location below the liquid
level. The improved method comprises introducing a separate
stream of said heavy petroleum oil into said thermal cracking
unit at said location below the liquid level, said stream
being introduced through an opening in said unit at a linear
velocity of not less than 5 cm/sec, measuring the pressure of
the oil being introduced and determining the liquid level
from the pressure measurement.

Revendications

The embodiments of the invention in which an exclusive
property or privilege is claimed are defined as follows:
1. In a method of determining the liquid level of a heavy
petroleum oil charge stock in a thermal cracking unit by
measuring the liquid pressure at a location below the
liquid level, the improvement which comprises:
introducing a separate stream of said heavy petroleum
oil into said thermal cracking unit at said location below
the liquid level, said stream being introduced through an
opening in said unit at a linear velocity of not less than
5 cm/sec, measuring the pressure of the oil being intro-
duced and determining the liquid level from the pressure
measurement.
2. A method according to claim 1 wherein said separate
stream is introduced through an enclosed chamber and a
nozzle having a diameter in the range of 5 to 7 mm, said
pressure being measured in said chamber.
3. A method according to claim 2 wherein the pressure
measurement in the chamber is made with a diaphragm type
pressure gauge.
4. A method according to claim 1, 2 or 3 wherein said
separate stream is introduced at a temperature in the
range of 150 to 200°C.
5. In a method of determining the liquid level of content
material in a reactor in which a heavy petroleum oil is
subjected to a thermal cracking, by measuring the liquid
pressure at a certain point below said liquid level, the
improvement comprising:
(a) providing chambered means for connection to a through-
hole of the reactor for introducing the petroleum oil into
the reactor;

(b) introducing said heavy petroleum oil through said
chambered means into said content material at a linear
velocity of not less than 5 cm/sec from the through-hole
provided at a certain predetermined location in a side of
said reactor while measuring the pressure at said through-
hole through which said heavy petroleum oil is introduced;
and
(c) calculating the liquid pressure of said content
material at the location of said through-hole from the
introducing rate and pressure of said heavy petroleum oil.

Description

FIELD OF THE INVENTION:
This invention relates to a novel method of deter-
mining the liquid level of a heavy petroleum oil charge stock
in a thermal cracking unit.
BACKGRO~ND OF THE INVENTION:
For determining the liquid level of a charge stock
contained in a vessel, there has been prevalently employed a
method in which the liquid pressure at a certain fixed spot
below the liquid level is measured and the liquid level is
calculated from the difference between the measured liquid
pressure and atmospheric pressure above the liquid level.
However, when this method is employed for determining the
liquid level in a thermal cracker for heavy petroleum oils
such as asphalt, coal tar, heavy oils, etc., it is found
difficult to measure the liquid pressure at a certain spot
below the liquid level, because the charge stock is of a high
temperature on the order of 400 to 500C and also such
material tends readily from coke. For instance, when a part
of the charge stock is removed from the reactor through an
opening in the reactor wall and is immediately contacted with
a pressure gauge (for example, a diaphragm type pressure gauge),
such pressure gauge may be damaged by high temperature of the
material which contacts and heats the pressure gauge, or the
wall opening may be blocked by build-up of coke therein.
The object of this invention, therefore, is to
provide a method which allows determination, in a very simple
and advantageous way, of the liquid level in a thermal cracking
unit for heavy petroleum oils, while avoiding the above problems.
Thus, according to the present invention, there is
3n provided an improved method oE determining the liquid level of
a heavy petroleum oil charge stock in a thermal cracking
- 2 - ~4

~5~
unit by measuring the liquid pressure at a location below the
liquid level. According to the improvement, a separate stream
of the heavy petroleum oil is introduced into the thermal
cracking unit at the location below the liquid level through
an opening in the unit at a linear velocity of not less than
5 cm/sec. The pressure of this oil being introduced is
measured and the liquid level is determined from the pressure
measurement.
BRIEF DESCRIPTION OF THE DRAWING:
The accompanying drawing is a schematic illustration
of a system for practicing the method of this invention.
DETAILED DESCRIPTION OF THE INVENTION:
A preferred embodiment of the present invention is
now described with reference to the accompanying drawing.
In the drawing, reference numeral 1 designates the
outer wall of a thermal cracking unit9 2 a nozzle, 3 a pipe,
4 castable bricks, 5 a flange, 6 a chamber into which a heavy
petroleum oil is introduced, 7 a pressure gauge, and 8 a heavy
; petroleum oil inlet. The heavy petroleum oil introduced
into the chamber 6 is of the same type as the heavy petroleum
oil which is subjected to a thermal cracking in the unit.
The pressure gauge 7 is preferably a diaphragm type pressure
gauge and this represents an important advantage of the
invention. (The diaphragm type pressure gauge has been considered
to be unsuitable for this use in the prior art). This pressure
gauge 7 communicates with the chamber 6, pipe 3 and nozzle 2.
In practicing the method according to this invention,
a heavy petroleum oil is introduced into the chamber 6 from
inlet 8 and then injected into the charge stock in the reactor
at a linear velocity of not less than 5 cm/sec from the nozzle
2, while measuring the introducing pressure. In this case, it

is preferable that the heavy petroleum oil introduced into
the chamber 6 has a temperature of 150 to 200C, more partic-
ularly a temperature of around 180C, so as not to exert any
undesirable influence to the thermal cracl;ing reaction of the
heavy petroleum oil in the reactor. The linear velocity of
the heavy petroleum oil injected into the charge stock in the
reactor from the nazzle 2 should be not less than 5 cm/sec
since a lower linear velocity than 5 cm/sec may cause coking of
the oil, resulting in blocking of the nozzle 2.
The size of the nozzle is also important. If it is
too small, there is a danger of it being blocked by coke
formation, while if it is too large the flow of the separate
stream of heavy oil entering the unit at this location may
upset the thermal cracking operation in the cracking unit.
Accordingly, the nozzle preferably has a bore in the range of
5 to 7 mm.
Example:
A vacuum residue of Khafji crude oil was subjected
to a thermal cracking in a reactor at a temperature of 400 to
~.50C and at a rate of 300 kg/hr to produce binder pitch. The
,~ reactor used here was equipped with a system such as shown in
i the accompanying drawing. The nozzle bore in the system was
6 mm.
In practicing the thermal cracking, tests were
conducted on the method of this invention by varying the linear
velocity of a separate inlet stream of the vacuum residue as
shown in the Table below. The test results are also shown
in the Table.
., ~

No. Flow rate Linear velocity Results
..
1 3 ~/hr 3 cm/sec Nozzle aperture was block-
ed after 40-hour operation
to make the system inope-
rative.
_ .
2 10 Q/hr 10 cm/sec Traces of coking -in the
nozzle aperture were found
after 700-hour operation.
_ . , ._. .. _
3 30 Q/hr 30 cm/sec No coking developed in the
nozzle aperture in 2000
hours of operation.
As is ap~arent ~rom the above .able, the nozzle hole was
blocked when the linear velocity was outside the range defined
in this invention (Test No. 1), whereas little or no coking
took place in the nozzle hole when the linear velocity was
within the defined range of this inVerltion (Test Nos. 2 and 3).
This very clearly in~icates that very long operational periods
are possible without problems when the ~Rthod of the invention
is followed.